JPH05239490A - Purification of hydraulic oil, and filter circuit used therefor - Google Patents

Purification of hydraulic oil, and filter circuit used therefor

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Publication number
JPH05239490A
JPH05239490A JP4044175A JP4417592A JPH05239490A JP H05239490 A JPH05239490 A JP H05239490A JP 4044175 A JP4044175 A JP 4044175A JP 4417592 A JP4417592 A JP 4417592A JP H05239490 A JPH05239490 A JP H05239490A
Authority
JP
Japan
Prior art keywords
hydraulic oil
solvent
filter
hydraulic
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP4044175A
Other languages
Japanese (ja)
Inventor
Yasunari Yoshie
耕也 吉江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP4044175A priority Critical patent/JPH05239490A/en
Publication of JPH05239490A publication Critical patent/JPH05239490A/en
Pending legal-status Critical Current

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  • Fluid-Pressure Circuits (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Lubricants (AREA)

Abstract

PURPOSE:To provide a method for purifying a hydraulic oil, which makes it possible to convert impurities dissolved in a hydraulic oil into a solid material for easy removal without using any chemical adsorption filter whose maintenance is troublesome, and to provide a filter circuit. CONSTITUTION:This method for purifying a hydraulic oil comprises the first processing step for introducing a hydraulic oil bypassed from an oil supply line 3 on the side of hydraulic device into a processing tank 9 to dilute in with a solvent, causing the impurities dissolved in the oil to deposit as a solid material in the liquid, the second processing step for passing the diluted hydraulic oil through a filter 10 to remove the solid impurities present in the diluted liquid, and the third processing step for sending the diluted liquid filtrated through the filter into distillation device 11 to effect distillation to thereby separate into a hydraulic oil and a solvent, wherein the hydraulic oil purified through the consecutive processing steps is returned to the oil supply line while the solvent evaporated in the distillation device is condensed by a subsequent condenser 12 and the returned to the processing tank for reuse.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、高圧油圧装置などに使
用するリン酸エステル系油圧油の油中に生成,混在する
不純物を除去する浄化方法,およびそのフィルタ回路に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a purification method for removing impurities produced in and mixed with a phosphate ester hydraulic oil used in a high-pressure hydraulic system, and a filter circuit therefor.

【0002】[0002]

【従来の技術】蒸気タービンの電気−油圧ガバナなどの
高圧油圧装置では、火災防止の面から油圧油として抗着
火性に優れ,かつ高温高圧に対しても性状変化の少ない
リン酸エステル系の油圧油が広く採用されている。とこ
ろで、かかるリン酸エステル系系の油圧油は使用中に周
囲からの水分混入,温度上昇などが原因でリン酸エステ
ルが劣化,分解し、油圧油中には不純物(酸,および酸
により腐蝕,溶解した生成物)が生成するようになる。
2. Description of the Related Art In a high-pressure hydraulic system such as an electro-hydraulic governor of a steam turbine, a phosphate ester type hydraulic system which is excellent in anti-ignition property as a hydraulic fluid from the viewpoint of fire prevention and has little property change under high temperature and high pressure. Oil is widely used. By the way, in such a phosphate ester type hydraulic fluid, the phosphate ester is deteriorated and decomposed due to mixing of moisture from the surroundings during use, temperature rise, etc., and impurities (acids and corrosion due to acid, A dissolved product) will be produced.

【0003】そこで、従来では油圧装置に図3で示すよ
うなフィルタ回路を組合わせ、油圧装置側からバイパス
させた油圧油をフィルタ回路に導いて金属粉,パッキン
屑などの固形異物とともに油圧油に溶解している不純物
を除去するようにしいてる。図において、1は油圧油タ
ンク、2は油圧油タンク1と油圧装置3との間に配管し
た給油ライン、4は油圧ポンプ、5はフィルタ回路であ
り、フィルタ回路5は化学的な吸着フィルタ6,機械式
のフィルタ7,循環ポンプ8で構成されている。
Therefore, conventionally, a hydraulic system is combined with a filter circuit as shown in FIG. 3, and hydraulic oil bypassed from the hydraulic system side is guided to the filter circuit to be converted into hydraulic oil together with solid foreign matters such as metal powder and packing scraps. Remove the dissolved impurities. In the figure, 1 is a hydraulic oil tank, 2 is an oil supply line piped between the hydraulic oil tank 1 and a hydraulic device 3, 4 is a hydraulic pump, 5 is a filter circuit, and the filter circuit 5 is a chemical adsorption filter 6 , A mechanical filter 7 and a circulation pump 8.

【0004】かかる構成で、給油ライン3からバイパス
させて取り込んだ油圧油をフィルタ回路5に流すことに
より、吸着フィルタ5で油中に溶解している不純物を除
去し、さらにフィルタ6で油圧油を濾過して金属粉,パ
ッキン屑などの固形夾雑物を除去し、浄化処理された油
圧油が再び給油ライン2に戻される。
With this structure, the hydraulic oil bypassed from the oil supply line 3 is flowed into the filter circuit 5, whereby the adsorption filter 5 removes impurities dissolved in the oil, and the filter 6 removes the hydraulic oil. The filtered hydraulic oil removes solid impurities such as metal powder and packing scraps, and the purified hydraulic oil is returned to the oil supply line 2 again.

【0005】[0005]

【発明が解決しようとする課題】ところで、リン酸エス
テル系油圧油に溶解している不純物を化学的に吸着除去
するには、その吸着条件が複雑で安定した能力を常時維
持させることが難しく、また吸着フィルタは使用経過に
伴う吸着能力の低下から頻繁にフィルタを交換する必要
があるほか、フィルタ交換に伴って多量の廃棄物が発生
するなど、その保守管理が極めて厄介であることからそ
の対策が望まれている。
By the way, in order to chemically adsorb and remove the impurities dissolved in the phosphate ester hydraulic oil, the adsorption conditions are complicated and it is difficult to always maintain a stable capacity. In addition, it is necessary to replace the adsorption filter frequently because the adsorption capacity deteriorates with use, and a large amount of waste is generated with the replacement of the filter. Is desired.

【0006】本発明は上記の点にかんがみなされたもの
であり、その目的は前記課題を解決し、保守管理の厄介
な化学的吸着フィルタを使用することなく、油圧油中に
溶解している不純物を固形物に変えて簡単に除去できる
ようにした油圧油の浄化方法,およびフィルタ回路を提
供することにある。
The present invention has been made in view of the above points, and an object thereof is to solve the above problems and to eliminate impurities dissolved in hydraulic fluid without using a chemical adsorption filter which is troublesome to maintain. (EN) It is intended to provide a method for purifying hydraulic oil, which can be easily removed by converting solids into solid matter, and a filter circuit.

【0007】[0007]

【課題を解決するための手段】上記目的は、本発明の浄
化方法により、油圧装置の給油ラインからバイパスさせ
た油圧油を溶剤で希釈し、油中に溶解している不純物を
固形物として析出させる第1の処理工程と、油圧油の希
釈液をフィルタに通して固形夾雑物を除去する第2の処
理工程と、フィルタで濾過した油圧油の希釈液を蒸溜し
て油圧油と溶剤とを分離させる第3の処理工程を有し、
前記の各処理工程を順に経て浄化した油圧油を給油ライ
ンに戻すことにより達成される。
According to the purification method of the present invention, the above-mentioned object is to dilute the hydraulic oil bypassed from the oil supply line of the hydraulic system with a solvent and to precipitate impurities dissolved in the oil as solid matter. The first treatment step is performed, and the second treatment step is performed in which the diluent for the hydraulic oil is passed through a filter to remove solid contaminants. The diluent for the hydraulic oil filtered by the filter is distilled to separate the hydraulic oil and the solvent. Has a third process step of separating,
This is achieved by returning the purified hydraulic oil to the oil supply line through the above processing steps in order.

【0008】また、前記浄化方法の実施には、次のよう
な実施態様がある。 (1)溶剤として、低分子量低沸点パラフィン系溶剤を
使用する。 (2)前記方法における第3の処理工程では、蒸発した
溶剤蒸気を凝縮させた後に第1の工程に戻して再使用す
る。 (3)前記第3の処理工程では、加熱蒸溜,もしくは減
圧蒸溜により溶剤を蒸発させて油圧油と分離する。
Further, there are the following modes for carrying out the cleaning method. (1) As a solvent, a low molecular weight low boiling point paraffinic solvent is used. (2) In the third treatment step of the above method, the evaporated solvent vapor is condensed and then returned to the first step for reuse. (3) In the third treatment step, the solvent is evaporated by heating distillation or reduced pressure distillation to separate from the hydraulic oil.

【0009】一方、前記浄化方法の実施に使用するフィ
ルタ回路は、本発明により、油圧装置の給油ラインから
取り込んだ油圧油を溶剤中に注入して希釈し、油中に溶
解している不純物を固形物として析出させる処理槽と、
該処理槽の後段に接続して油圧油の希釈液を濾過するフ
ィルタと、フィルタの後段に接続して油圧油と溶剤とを
分離させる蒸溜装置と、蒸溜装置と前記処理槽との間に
接続して油圧油と分離した溶剤蒸気を凝縮させるコンデ
ンサを組合わせて構成するものとする。
On the other hand, according to the present invention, the filter circuit used for carrying out the above-mentioned purification method is designed to inject and dilute the hydraulic oil taken in from the oil supply line of the hydraulic device into the solvent to remove impurities dissolved in the oil. A treatment tank for depositing a solid matter,
A filter connected to the latter stage of the treatment tank to filter the diluting fluid of the hydraulic oil, a distillation device connected to the latter stage of the filter to separate the hydraulic oil and the solvent, and connected between the distillation device and the treatment tank. Then, a condenser for condensing the solvent vapor separated from the hydraulic oil is combined and configured.

【0010】また、前記フィルタ回路における蒸溜装置
としては、加熱蒸溜装置,あるいは減圧蒸溜装置を採用
して実施することができる。
Further, as the distilling device in the filter circuit, a heating distilling device or a reduced pressure distilling device can be adopted.

【0011】[0011]

【作用】上記のフィルタ回路を通じてリン酸エステル系
油圧油を浄化することにより、リン酸エステル系の劣化
などで油圧油中に生成した溶解不純物は、第1の処理工
程における油圧油の溶剤希釈,冷却により固形物に変わ
って液中に析出するようになる。したがって次の第2処
理工程では析出不純物が他の固形異物と一緒に固形夾雑
物としてフィルタの濾過により除去される。一方、不純
物が除去された油圧油と溶剤との混合液は続く第3の処
理工程で蒸溜処理され、ここで油圧油に比べて沸点の低
い溶剤が蒸発して油圧油と分離した後、油圧油は油圧装
置の給油ラインに戻され、溶剤蒸気は凝縮させた後に再
び第1の処理工程に戻して再使用される。なお、前記の
第1処理工程で、溶剤の種類,希釈率,処理温度を適切
に選定するにより、油圧油中の不純物生成状態に対応し
て浄化処理を効率的に行うことができる。また、油圧油
の浄化処理工程の途中で適宜不凝縮ガスを系外に抜き取
りことにより、同時に水蒸気として混在している水分の
除去も可能となる。
By cleaning the phosphate ester hydraulic oil through the above filter circuit, the dissolved impurities generated in the hydraulic oil due to the deterioration of the phosphate ester type are dissolved in the hydraulic fluid in the first treatment step by solvent dilution, Upon cooling, it turns into a solid and begins to precipitate in the liquid. Therefore, in the next second treatment step, the precipitated impurities, together with other solid foreign matters, are removed as solid impurities by filtration through the filter. On the other hand, the mixed liquid of the hydraulic oil from which the impurities have been removed and the solvent is distilled in the subsequent third treatment step, where the solvent having a lower boiling point than the hydraulic oil evaporates and is separated from the hydraulic oil. The oil is returned to the oil supply line of the hydraulic system, and the solvent vapor is condensed and then returned to the first processing step for reuse. By appropriately selecting the type of solvent, the dilution rate, and the treatment temperature in the first treatment step, the purification treatment can be efficiently performed according to the state of impurities generated in the hydraulic oil. Further, by appropriately extracting the non-condensable gas to the outside of the system during the hydraulic oil purification process, it is possible to simultaneously remove water mixed as water vapor.

【0012】[0012]

【実施例】以下本発明の実施例を図面に基づいて説明す
る。なお、実施例の図中で図3と対応する同一部材には
同じ符号が付してある。 実施例1:図1において、9は例えば低分子低沸点パラ
フィン系の溶剤(例えば沸点40〜80度程度)を貯留
した処理槽、10は濾材を用いた機械式のフィルタ、1
1は加熱蒸溜装置、12は溶剤凝縮用のコンデンサ、1
3は送液ポンプであり、これらの各機器の相互間,給油
ライン3との間に油圧油抽出管路14,油圧油戻し管路
15,溶剤戻し管路16を図示のように配管して油圧油
の浄化装置を構成している。なお、11aは加熱蒸溜装
置11の加熱ヒータ、17はドレンポットである。
Embodiments of the present invention will be described below with reference to the drawings. In the drawings of the embodiments, the same members as those in FIG. 3 are designated by the same reference numerals. Example 1 In FIG. 1, 9 is a processing tank in which a low molecular weight low boiling point paraffinic solvent (for example, a boiling point of about 40 to 80 degrees) is stored, 10 is a mechanical filter using a filter medium, 1
1 is a heating distillation apparatus, 12 is a condenser for condensing a solvent, 1
Reference numeral 3 is a liquid feed pump, and a hydraulic oil extraction pipe line 14, a hydraulic oil return pipe line 15, and a solvent return pipe line 16 are connected as shown in the drawing between the respective equipments and between the oil supply line 3. It constitutes a device for purifying hydraulic oil. In addition, 11a is a heater of the heating distillation apparatus 11, and 17 is a drain pot.

【0013】かかる構成で、油圧装置の運転時に給油ラ
イン3の供給側管路(高圧側)からバイパスさせた油圧
油を抽出管路14を通じて処理槽9に注入すると、処理
槽で油圧油が溶剤で希釈される。ここで処理槽9での希
釈率,冷却温度を適正に調節することにより、油圧油中
に溶解している不純物は油圧油の希釈液中に固形物とし
て析出される。そして、液中に析出した固形物,他の混
入固形異物は油圧油の希釈液とともに送液ポンプ13に
より処理槽9から後段のフィルタ10に送り込まれ、こ
こで不純物が固形夾雑物としてフィルタでの濾過により
除去される。一方、フィルタ10で濾過された油圧油の
希釈液は後段の加熱蒸溜装置11に入り、低沸点の溶剤
が加熱蒸発して油圧油と分離する。また、ここで分離し
た油圧油は蒸溜装置11より取り出され、油圧油戻し管
路15を経て給油ライン3の戻り側管路(低圧側)に還
流する。一方、蒸溜装置11で蒸発した溶剤蒸気は後段
のコンデンサ12で凝縮した後、処理槽9に送り込まれ
て再使用される。
With such a configuration, when the hydraulic oil bypassed from the supply side pipeline (high pressure side) of the oil supply line 3 is injected into the processing tank 9 through the extraction pipeline 14 during operation of the hydraulic system, the hydraulic oil is converted into solvent in the processing tank. Diluted with. By appropriately adjusting the dilution ratio and cooling temperature in the processing tank 9, the impurities dissolved in the hydraulic fluid are deposited as solids in the hydraulic fluid diluent. Then, the solid matter precipitated in the liquid and other mixed solid foreign matters are sent from the processing tank 9 to the filter 10 in the subsequent stage by the liquid sending pump 13 together with the hydraulic fluid diluting liquid, where the impurities are solid impurities in the filter. Removed by filtration. On the other hand, the diluting liquid of the hydraulic oil filtered by the filter 10 enters the heating / distilling device 11 in the subsequent stage, and the low boiling point solvent is heated and evaporated to be separated from the hydraulic oil. Further, the hydraulic oil separated here is taken out from the distilling device 11 and is returned to the return side pipeline (low pressure side) of the oil supply line 3 via the hydraulic oil return pipeline 15. On the other hand, the solvent vapor evaporated in the distillation apparatus 11 is condensed in the condenser 12 at the subsequent stage, and then sent to the processing tank 9 for reuse.

【0014】実施例2:図2は先記した実施例1の応用
実施例を示すものであり、この実施例では図1における
加熱蒸溜装置の代わりに減圧蒸溜装置18が組み込まれ
ている。なお、19は油圧油の戻しポンプ、20は溶剤
蒸気の送気用コンプレッサである。かかる構成による油
圧油の浄化処理は基本的に実施例1と同様に行われる。
一方、図2の実施例では処理槽9はコンプレッサ19に
より加圧されており、この圧力により処理槽9から油圧
油の希釈液がフィルタ10を経て減圧蒸溜装置18に送
り込まれ、溶剤が減圧蒸発して油圧油と分離する。ま
た、蒸溜装置18から取り出された油圧油は戻しポンプ
20で昇圧した後に戻し管路15を経て油圧装置側の給
油ライン3に戻される。
Example 2 FIG. 2 shows an application example of Example 1 described above. In this example, a vacuum distillation apparatus 18 is incorporated in place of the heating distillation apparatus in FIG. Reference numeral 19 is a hydraulic oil return pump, and 20 is a solvent vapor compressor. The hydraulic oil purifying process with such a configuration is basically performed in the same manner as in the first embodiment.
On the other hand, in the embodiment shown in FIG. 2, the processing tank 9 is pressurized by the compressor 19, and this pressure causes the diluent of hydraulic oil to be sent from the processing tank 9 through the filter 10 to the depressurizing distillation apparatus 18 to evaporate the solvent under reduced pressure. And separate it from hydraulic oil. Further, the hydraulic oil taken out from the distilling device 18 is returned to the oil supply line 3 on the hydraulic device side through the return pipe 15 after the pressure is increased by the return pump 20.

【0015】[0015]

【発明の効果】以上述べたように、本発明による油圧油
の浄化方法,装置によれば、リン酸エステル系の油圧油
中に溶解している不純物を、油圧油を溶剤で希釈するこ
とにより液中に固形物として析出することができ、これ
により不純物を固形夾雑物として後段の機械式フィルタ
で濾過して容易に取り除くことができる。しかも、不純
物を固形物として除去するようにしたので、従来の化学
的な吸着式フィルタと比べて安定した処理機能が維持で
き、かつフィルタも長く使用できるほかフィルタの交換
に伴う廃棄物の発生量も少なくて済むなど保守管理も簡
単となるなどの利点が得られる。また、溶剤は蒸溜装置
で油圧油と分離した後、凝縮して再び処理槽に戻して使
用するようにしたので消耗量も少なくて済む。
As described above, according to the method and apparatus for purifying hydraulic oil of the present invention, impurities dissolved in phosphate ester hydraulic oil can be diluted by diluting the hydraulic oil with a solvent. It can be precipitated as a solid in the liquid, and thus impurities can be easily removed as solid impurities by filtration with a mechanical filter in the subsequent stage. Moreover, since impurities are removed as solids, a stable treatment function can be maintained compared to conventional chemical adsorption filters, and the filter can be used for a long time. The advantages are that maintenance management is easy, such as less is required. Further, the solvent is separated from the hydraulic oil by the distilling device and then condensed and returned to the processing tank for use, so that the consumption amount is small.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施例によるフィルタ回路の構成図FIG. 1 is a configuration diagram of a filter circuit according to an embodiment of the present invention.

【図2】図1と異なる本発明実施例のフィルタ回路の構
成図
FIG. 2 is a block diagram of a filter circuit according to an embodiment of the present invention, which is different from FIG.

【図3】従来におけるフィルタ回路の構成図FIG. 3 is a block diagram of a conventional filter circuit.

【符号の説明】[Explanation of symbols]

1 油圧油タンク 3 給油ライン 9 処理槽 10 フィルタ 11 加熱蒸溜装置 12 コンデンサ 18 減圧蒸溜装置 1 Hydraulic Oil Tank 3 Oil Supply Line 9 Processing Tank 10 Filter 11 Heating Distillation Device 12 Condenser 18 Decompression Distillation Device

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】油圧装置で使用するリン酸エステル系の油
圧油中生成,混在する不純物を除去する油圧油の浄化方
法であって、油圧装置側の給油ラインからバイパスさせ
た油圧油を溶剤で希釈し、油中に溶解している不純物を
固形物として析出させる第1の処理工程と、油圧油の希
釈液をフィルタに通して固形夾雑物を除去する第2の処
理工程と、フィルタで濾過した油圧油の希釈液を蒸溜し
て油圧油と溶剤とを分離させる第3の処理工程を有し、
前記の各処理工程を順に経て浄化した油圧油を給油ライ
ンに戻すことを特徴とする油圧油の浄化方法。
1. A method of purifying a hydraulic oil, which is produced in a phosphate ester hydraulic oil used in a hydraulic system and removes mixed impurities, wherein the hydraulic oil bypassed from an oil supply line on the hydraulic system side with a solvent. A first treatment step for diluting and precipitating impurities dissolved in oil as a solid matter, a second treatment step for removing a solid contaminant by passing a diluent of hydraulic oil through a filter, and a filtration with a filter And a third treatment step for distilling the diluted fluid of the hydraulic oil to separate the hydraulic oil and the solvent.
A method of purifying hydraulic oil, characterized in that the hydraulic oil purified through the above-mentioned processing steps is returned to the oil supply line.
【請求項2】請求項1記載の浄化方法において、溶剤が
低分子量低沸点パラフィン系溶剤であることを特徴とす
る油圧油の浄化方法。
2. The method for purifying hydraulic oil according to claim 1, wherein the solvent is a low molecular weight low boiling point paraffinic solvent.
【請求項3】請求項1記載の浄化方法において、第3の
処理工程で蒸発した溶剤蒸気を凝縮させ、第1の処理工
程に戻して再使用することを特徴とする油圧油の浄化方
法。
3. The method for purifying hydraulic oil according to claim 1, wherein the solvent vapor evaporated in the third treatment step is condensed and returned to the first treatment step for reuse.
【請求項4】請求項1記載の浄化方法において、第3の
処理工程では、加熱蒸溜により溶剤を加熱蒸発させて油
圧油と分離することを特徴とする油圧油の浄化方法。
4. The method for purifying hydraulic oil according to claim 1, wherein in the third treatment step, the solvent is heated and evaporated by heating distillation to separate the solvent from the hydraulic oil.
【請求項5】請求項1記載の浄化方法において、第3の
処理工程では、減圧蒸溜により溶剤を減圧蒸発させて油
圧油と分離することを特徴とする油圧油の浄化方法。
5. The method for purifying hydraulic oil according to claim 1, wherein in the third treatment step, the solvent is evaporated under reduced pressure by vacuum distillation to separate the solvent from the hydraulic oil.
【請求項6】油圧装置の給油ラインから取り込んだ油圧
油を溶剤中に注入して希釈し、油中に溶解している不純
物を固形物として析出させる処理槽と、該処理槽の後段
に接続して油圧油の希釈液を濾過するフィルタと、フィ
ルタの後段に接続して油圧油と溶剤とを分離させる蒸溜
装置と、蒸溜装置と前記処理槽との間に接続して油圧油
と分離した溶剤蒸気を凝縮させるコンデンサを組合わせ
てなる請求項1記載の浄化方法の実施に使用する油圧油
のフィルタ回路。
6. A treatment tank for injecting hydraulic oil taken in from a refueling line of a hydraulic device into a solvent to dilute it and depositing impurities dissolved in the oil as a solid matter, and a treatment tank connected to the latter stage of the treatment tank. A filter for filtering the diluted fluid of hydraulic oil, a distilling device connected to the latter stage of the filter to separate hydraulic oil and solvent, and a distilling device connected to the processing tank to separate hydraulic oil. A hydraulic oil filter circuit used for carrying out the purification method according to claim 1, wherein a condenser for condensing solvent vapor is combined.
【請求項7】請求項6記載の浄化装置において、蒸溜装
置が加熱蒸溜装置であることを特徴とする油圧油のフィ
ルタ回路。
7. A filter circuit for hydraulic oil according to claim 6, wherein the distilling device is a heating distilling device.
【請求項8】請求項6記載の浄化装置において、蒸溜装
置が減圧蒸溜装置であることを特徴とする油圧油のフィ
ルタ回路。
8. A filter circuit for hydraulic oil according to claim 6, wherein the distillation device is a vacuum distillation device.
JP4044175A 1992-03-02 1992-03-02 Purification of hydraulic oil, and filter circuit used therefor Pending JPH05239490A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4044175A JPH05239490A (en) 1992-03-02 1992-03-02 Purification of hydraulic oil, and filter circuit used therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4044175A JPH05239490A (en) 1992-03-02 1992-03-02 Purification of hydraulic oil, and filter circuit used therefor

Publications (1)

Publication Number Publication Date
JPH05239490A true JPH05239490A (en) 1993-09-17

Family

ID=12684247

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4044175A Pending JPH05239490A (en) 1992-03-02 1992-03-02 Purification of hydraulic oil, and filter circuit used therefor

Country Status (1)

Country Link
JP (1) JPH05239490A (en)

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Cited By (6)

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Publication number Priority date Publication date Assignee Title
JP2001276504A (en) * 2000-03-29 2001-10-09 Chuyu Shoji Kk Recycle system for recovery and treatment of organic- solvent waste liquid
KR100419287B1 (en) * 2000-10-04 2004-02-14 세퍼레이션디자인테크(주) Tramp Oil Separator with sterilization
CN104454796A (en) * 2014-11-02 2015-03-25 中冶东方工程技术有限公司 Oil supplementation system
JP2018167210A (en) * 2017-03-30 2018-11-01 株式会社Ihi Distillation apparatus
RU2698995C1 (en) * 2019-03-11 2019-09-02 Федеральное государственное бюджетное образовательное учреждение высшего образования "Казанский государственный аграрный университет" (ФГБОУ ВО Казанский ГАУ) Internal lubrication system of turbo compressor bearing assembly of internal combustion engine
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